US2008132733A1PendingUtilityA1

Process for making dibutyl ethers from aqueous 2-butanol

Assignee: MANZER LEO ERNESTPriority: Dec 1, 2006Filed: Jun 13, 2007Published: Jun 5, 2008
Est. expiryDec 1, 2026(~0.3 yrs left)· nominal 20-yr term from priority
C07C 41/09C07C 41/42
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Claims

Abstract

The present invention relates to a catalytic process for making dibutyl ethers using a reactant comprising 2-butanol and water. The dibutyl ethers so produced are useful in transportation fuels.

Claims

exact text as granted — not AI-modified
1 . A process for making at least one dibutyl ether comprising contacting a reactant comprising 2-butanol and at least about 5% water (by weight relative to the weight of the water plus 2-butanol) with at least one acid catalyst at a temperature of about 50 degrees C. to about 450 degrees C. and a pressure from about 0.1 MPa to about 20.7 MPa to produce a reaction product comprising said at least one dibutyl ether, and recovering said at least one dibutyl ether from said reaction product to obtain at least one recovered dibutyl ether. 
     
     
         2 . The process of  claim 1 , wherein the reactant is obtained from a fermentation broth. 
     
     
         3 . The process of  claim 2 , wherein the reactant is obtained by subjecting the fermentation broth to a refining process that comprises at least one step selected from the group consisting of pervaporation, gas-stripping, adsorption, liquid-liquid extraction, distillation and molecular sieves. 
     
     
         4 . The process of  claim 3 , wherein said distillation produces a vapor phase having a water concentration of at least about 27% (by weight relative to the weight of the water plus 2-butanol), and wherein the vapor phase is used as the reactant. 
     
     
         5 . The process of  claim 3 , wherein said distillation produces a vapor phase having a water concentration of at least about 27% (by weight relative to the weight of the water plus 2-butanol), wherein the vapor phase is condensed to produce a liquid phase, and wherein the liquid phase is used as the reactant. 
     
     
         6 . The process of  claim 1  or  claim 4 , wherein the at least one acid catalyst is a heterogeneous catalyst, and the temperature and the pressure are chosen so as to maintain the reactant and the reaction product in the vapor phase.

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